CN204534605U - The liquid waste incineration boiler of the adherent protection of a kind of flue gas recycled - Google Patents
The liquid waste incineration boiler of the adherent protection of a kind of flue gas recycled Download PDFInfo
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Abstract
The utility model relates to liquid waste disposal technique field, is specifically related to the liquid waste incineration boiler of the adherent protection of a kind of flue gas recycled.This boiler comprises the descending adiabatic furnace, radiant cooling room, horizontal flue and the back-end ductwork that are connected successively, and is arranged at the soot blower on radiant cooling room, horizontal flue and back-end ductwork; Back-end ductwork is provided with I grade, II grade of economizer etc.The partial fume at II grade of economizer exit place recycles by the utility model, enters descending adiabatic furnace and radiant cooling room as adherent protection flue gas; Between descending adiabatic furnace and radiant cooling room, junction is V-arrangement angle, and the sidewall of V-arrangement angle is water-cooling wall, and water-cooling wall is equipped with refractory material, and the bottom of V-arrangement angle is liquid state slag discharging device.Burning boiler described in the utility model, solves that boiler wall burn into deslagging is smooth, NOx discharge crosses the problems such as high well, has the advantages such as structure is simple, easy to use, treatment effeciency is high, energy-saving water-saving.
Description
Technical field
The utility model relates to liquid waste disposal technique field, is specifically related to the high concentration salty organic waste liquid burning boiler of the adherent protection of a kind of flue gas recycled.
Background technology
High concentrated organic waste liquid is extensively present in the industries such as basic chemical feedstock manufacture, Coal Chemical Industry, petrochemical industry.The total emission volumn of China's waste water (liquid) is in rising trend in nearly 5 years, and wherein industrial wastewater (liquid) is the primary pollution source of China's water environment pollution.The industrial wastewater (liquid) that China discharges every year accounts for about 50% of waste water (liquid) total emission volumn.Therefore, research application is carried out to the processing method of high concentrated organic waste liquid and there is very real meaning.Not only organic concentration is high for high concentrated organic waste liquid, toxicity large, complicated component, and containing a large amount of alkali metal inorganic salt and other material, but also there is the organic matter much can not degraded.In Biochemical method process, high concentration bases and alkaline metal salt material have very strong inhibitory action to microorganism, and general materialization or materialization-biochemistry method are difficult to removing.Therefore, burning method processes the topmost technical method of this type of waste liquid at present.Burning disposal organic liquid waste is a kind of simple, efficient, feasible method; it is recoverable partial heat, reduction processing cost both; pollutant can be carried out harmless treatment again; reduce the generation of new polluter as far as possible; avoid causing secondary pollution, reach the dual purpose of comprehensive utilization of waste materials and protection of the environment.
Now, burning disposal organic liquid waste normally adopts liquid waste incinerator.Burned by liquid waste incinerator, non-toxic gas waste liquid being decomposed in combustion can enter air is (as CO
2) or by smoke eliminator absorb gas (as SO
2), make the non-combustible one-tenth separating/enriching in waste liquid become lime-ash and trap.Owing to containing a large amount of moisture in waste liquid, calorific value is lower, flammable poor, therefore needs in burning process to use the temperature in combustion-supporting fuel raising burner hearth, ensures the rapid evaporation of moisture and the complete combustion decomposition of combustible component in waste liquid.Inorganic salts also containing high concentration in waste liquid, in burning process, the alkali metal salt in waste liquid is formed has corrosive liquid slag, causes corrosion, affect the continuous operation of incinerator to burner hearth refractory material and boiler heating surface.And when and Flow Field Distribution of burner hearth higher when alkali metal salt content is unreasonable, the problem such as also easily cause deslagging not smooth.Because in part chemical waste liquid, nitrogen content is higher, therefore, effectively controls NOx generation and discharge and also become problem demanding prompt solution.
The general burning boiler of current employing is less relative to treating capacity, waste liquid time of staying in burner hearth is relatively short, it is not thorough that organic matter burns reaction, corrosivity alkali metal salt containing higher concentration in flue gas, easy slagging scorification dust stratification, causes corrosion to boiler wall, due to chamber structure and Flow Field Distribution unreasonable, cause deslagging not smooth, make the steady and continuous cycle of operation shorter.
Chinese patent application CN101078520A proposes a kind of high concentration organic waste liquid burning device, comprise two incinerator, expansion chamber, waste heat recovery workshop section, scrubbing tower, knockout drum, air-introduced machine and chimney, wherein, the middle lower end of the top of first incinerator and second incinerator is provided with combustor, and two incinerators pass through pipeline communication in bottom.This liquid waste incinerator described in application has following shortcoming when burning waste liquid: the part that bottom between (1) two incinerator connects is H-shaped, the flame fullness degree of burner hearth bottom is poor, and liquid slag easily causes deslagging not smooth in the accumulation of burner hearth bottom and connecting pipe; (2) owing to not having adherent protection wind, the salt of melting is very easily bonded on wall, forms slagging scorification and causes corrosion to burner hearth wall; (3) owing to only arranging one-level auxiliary burner and not carrying out flue gas recirculation, control combustion regional temperature is unfavorable for, and then uncontrollable NO
xgeneration.
Chinese patent application CN102588980A proposes a kind of incineration boiler for saline waste liquid, comprises burner, liquid waste spray gun, adiabatic furnace combustion chamber, radiant cooling room, upper drum (drum), lower drum, convection bank, ash dropping hopper, furnace wall and steelframe.This liquid waste incinerator described in application has following shortcoming: (1) burning boiler adopts up burner hearth, and flue gas flow direction and lime-ash direction of landing is contrary, and high-temperature flue gas carries molten ash and enters back-end ductwork, causes corrode and dust stratification heating surface; (2) owing to not having adherent protection wind, the salt of melting is very easily bonded on wall, forms slagging scorification and causes corrosion to burner hearth wall; (3) only arrange one-level auxiliary burner and there is no flue gas recirculation, being unfavorable for control combustion regional temperature, and then uncontrollable NO
xgeneration.
Chinese patent application CN103047659A proposes a kind of process high concentration salty organic waste liquid burning boiler, comprises descending adiabatic furnace, multi-stage irradiation cooling chamber, convection heat-exchange chamber, soot blower, carbonated drink fairlead and drum.This application described in liquid waste incinerator there is following shortcoming: (1) descending adiabatic furnace is at the bottom of block furnace, and does not arrange furnace arch, furnace nose, furnace bottom be difficult to is washed into by high-temperature flue gas, lime-ash easily cools accumulation at furnace bottom, not easily discharges smoothly; (2) air-supply arrangement as shield gas flow is arranged in burner hearth corner, be difficult to be subject to most flue gas carry liquid slag corrosion burner hearth wall formed available protecting, and because send into be air, combustion zone oxygen content and then control combustion temperature can not be reduced, can not the generation of effective control NOx; (3) descending adiabatic furnace size is comparatively large, and does not have air preheater to carry out preheating to air, Thermal load of cross-section and volume heat load little, boiler cost is higher.
Chinese patent application CN101839474A proposes a kind of method for re-circulating combustion of flue gas of pulverized coal fired boiler, be applied to pulverized-coal fired boiler, this application described in combustion method be: (1) is at ignition combustion phase, utilize circulating flue gas to burner hearth pulverized coal conveying, the oxygen being separated air gained is sent into igniter simultaneously; (2) component loops flue gas is sent into burner hearth entrance, enter burner hearth with after oxygen mix; Carry coal dust with another part circulating flue gas and enter burner hearth.This flue gas recycled described in application does not enter burner hearth as adherent protection wind, can not solve the problem of wet bottom boiler burner hearth wall corrosion.
Because above-mentioned prior art all comes with some shortcomings, therefore, research and develop a kind ofly can solve that boiler wall burn into deslagging is smooth well, organic waste liquid containing salt burning boiler that NOx discharge crosses the problem such as high becomes a problem demanding prompt solution.
Summary of the invention
In order to overcome the deficiencies in the prior art, the utility model provides the high concentration salty organic waste liquid burning boiler of the adherent protection of a kind of flue gas recycled.
This burning boiler mainly comprises the descending adiabatic furnace, radiant cooling room, horizontal flue and the back-end ductwork that are connected successively, and is arranged at the soot blower on radiant cooling room, horizontal flue and back-end ductwork; Soot blower is for removing the Slag and accumulating ash on boiler heating surface;
The end face of described descending adiabatic furnace is provided with Waste liquid atomization spray gun and root wind snout, and top is provided with assisted gas burner I, and middle part is provided with assisted gas burner II, Hou Qiang bottom and is provided with furnace arch, furnace nose;
The porch of described radiant cooling room is provided with screen tube, and top is provided with E font water-cooling screen;
Described horizontal flue is provided with convection current screen;
Described back-end ductwork is disposed with II grade of economizer, plate air preheater and I grade of economizer from the inlet to the outlet, and the air outlet slit of plate air preheater is connected with root wind snout;
The feature of described burning boiler is: recycled by the partial fume at II grade of economizer exit place, enter descending adiabatic furnace and radiant cooling room as adherent protection flue gas; Between described descending adiabatic furnace and radiant cooling room, junction is V-arrangement angle, and the sidewall of V-arrangement angle is water-cooling wall, and water-cooling wall is equipped with refractory material, and the bottom of V-arrangement angle is liquid state slag discharging device.
Preferably, described adherent protection flue gas accounts for 10 ~ 25% of total exhaust gas volumn.
Preferably, described adherent protection flue gas is all adherent along flow of flue gas direction enters descending adiabatic furnace and radiant cooling room.
Preferably, described adherent protection flue gas is made up of I grade-IV grade adherent protection flue gas; I grade of adherent protection flue gas, II grade of adherent protection flue gas enter descending adiabatic furnace from the burner hearth wall below assisted gas burner I and assisted gas burner II respectively; III grade of adherent protection flue gas enters descending adiabatic furnace from the top of described V-arrangement angle; IV grade of adherent protection flue gas enters radiant cooling room from the bottom of described V-arrangement angle.
Preferably, the low 6 ~ 10m of aspect ratio radiant cooling room of described descending adiabatic furnace.
Preferably, laying place of described refractory material is 3 ~ 5m with the distance bottom V-arrangement angle.
Preferably, the interior angle of described V-arrangement angle is 60 ° ~ 90 °.Preferred, the interior angle of described V-arrangement angle is 70 ° ~ 85 °
Preferably, described screen tube is arranged by four the Crust blocks pipe bundle be staggered in arrangement and is formed.
Preferably, between the screen of described E font water-cooling screen, spacing is greater than 400mm.
Preferably, the carbonated drink outlet of described I grade of economizer, II grade of economizer, water-cooling wall, E font water-cooling screen, convection current screen is connected with drum with carbonated drink fairlead by header, drum is connected with down-comer, and the carbonated drink entrance that the carbonated drink outlet of down-comer is shielded with water-cooling wall, E font water-cooling screen, convection current is again connected.
In the utility model, atomization waste liquid sprays into from the top of descending adiabatic furnace under the parcel of root wind, the assisted gas burner I arranged on descending adiabatic furnace top and middle part and assisted gas burner II, adopt assisted gas fractional combustion, make burner hearth be divided into dry section and combustion zone, ensure that waste liquid is dry and burn completely in burner hearth different temperatures region.Upper furnace assisted gas burner I region is oxygen deprivation fuel-rich regions, be the dry section of waste liquid, assisted gas burner II region is the combustion zone of waste liquid, adopt flue gas recirculating technique and according to the burning feature staged air distribution in each district, dry section temperature is made to control at about 500 ~ 700 DEG C, combustion zone maximum combustion temperature reaches about 1200 DEG C, improves efficiency of combustion, reduces NO
xgeneration.
The partial fume at II grade of economizer exit place is carried out flue gas recirculation, is divided into four branch roads to enter burner hearth and cooling chamber as adherent protection wind, sprays into along flow of flue gas direction is adherent.Wherein, I grade of adherent protection flue gas sprays into the below of assisted gas burner I is adherent, the incomplete combustion that the waste liquid mainly preventing top from spraying into is adherent and cause, and reduce combustion zone oxygen concentration by circulating flue gas, play the effect of heat absorption body, control combustion temperature, thus make waste liquid dry and suppress the generation of nitrogen oxide, II grade of adherent protection flue gas, III grade of adherent protection flue gas and IV grade of adherent protection flue gas are respectively below assisted gas burner II, the top of V-arrangement angle and bottom spray into along flow of flue gas direction is adherent, flue gas recycled not only can suppress liquid slag to the direct contact of wall and corrosion as airflow layer, but also because it is different from the oxygen content characteristic of air, burner hearth wall is made to form hypothermia and hypoxia district in combustion zone, control oxygen concentration and ignition temperature, reduce the generation of NOx, in addition, utilize hypothermia and hypoxia district that adherent liquid slag cooled and solidified is formed solid slag protective layer at wall, isolated wall contacts with the direct of liquid slag, realize with slag anti-slag.
The Hou Qiang bottom of descending adiabatic furnace is provided with furnace arch, furnace nose, furnace arch, furnace nose is outstanding to burner hearth center, improve the degree of filling of flue gas in burner hearth, making flue gas even in the distribution trend of descending adiabatic furnace, preventing furnace bottom because high-temperature flue gas washes away the clogging phenomenon produced less than causing lime-ash to cool.
The V-arrangement angle of descending adiabatic furnace and radiant cooling room junction, the V-arrangement turn-around zone that high-temperature flue gas is diminished at flow area swerves, utilize liquid slag different with gas inertia, realize the inertial separation to liquid slag, the separated liquid slag got off gravitate on the furnace bottom tilted is discharged smoothly.Not at the lime-ash of V-arrangement angle inertial separation after speed slows down, flow through the screen tube in descending adiabatic furnace and exit, radiant cooling room turning, lime-ash in flue gas flows through the Crust blocks pipe bundle be staggered in arrangement, stick to screen tube surface, when melting ash deposition to a certain extent after, fall under gravity into burner hearth bottom and discharge.
In order to ensure that waste liquid can rapid draing burning in burner hearth, arrange plate air preheater at back-end ductwork, combustion air sends into burner hearth after air preheater is heated to 250 ~ 300 DEG C; Waste liquid, in the atomization of roof of the furnace center, adopts quadrangle tangential circle assisted combustion techniques, increases the contact area of waste liquid and thermal-flame, strengthen waste liquid and assisted gas to flow disturbance; Descending adiabatic furnace adopts less size, improves Thermal load of cross-section and the volume heat load of burner hearth, reduces boiler cost; 3 ~ 5 meters of lay refractory material at the water-cooling wall of V-arrangement angle apart from bottom simultaneously, ensure the time of staying of waste liquid at high-temperature area; Flue gas is by after heat exchanger heat exchange at different levels in radiant cooling room, horizontal flue, back-end ductwork, and exhaust gas temperature enters next stage flue gas processing device after dropping to design load.
In sum, the beneficial effects of the utility model are:
(1) efficiency of combustion is high, and have excellent treatment effect to high concentration saliferous organic hazardous waste liquid, disposal ability is greater than 10t/h, and pollutant emission is low, meets national environmental standard;
(2) rational steam parameter is selected, optimize stove combustion tissue, chamber structure and heating surface to arrange, solve molten alkali metal salt pair furnace wall and to cause bottom burn into the problems such as the smooth and back-end surfaces dust stratification of deslagging, device continous-stable, the cycle of operation are long;
(3) burn the waste heat produced can recycle, and produce steam, burn waste liquid energy byproduct steam per ton about 1.3 tons, reach the effective of resource and recycle.
Accompanying drawing explanation
Fig. 1 is the structural representation of the utility model burning boiler.
Number in the figure:
The descending adiabatic furnace of 1-; 11-Waste liquid atomization spray gun; 12-root wind snout; 13-assisted gas burner I; 14-assisted gas burner II; 15-furnace arch, furnace nose; The adherent protection flue gas of 16-I grade; The adherent protection flue gas of 17-II grade; 2-V clevis angle; 21-water-cooling wall; 22-refractory material; 23-liquid state slag discharging device; The adherent protection flue gas of 24-III grade; The adherent protection flue gas of 25-IV grade; 3-radiant cooling room; 31-screen tube: 32-E font water-cooling screen: 4-horizontal flue; 41-convection current is shielded: 5-back-end ductwork; 51-II grade of economizer; 52-plate air preheater; 53-I grade of economizer; 6-soot blower; 7-header; 8-carbonated drink fairlead; 9-drum; 10-down-comer.
Detailed description of the invention
The utility model provides the high concentration salty organic waste liquid burning boiler of the adherent protection of a kind of flue gas recycled, is described further the utility model below in conjunction with accompanying drawing.As shown in Figure 1, this burning boiler mainly comprises the descending adiabatic furnace 1, radiant cooling room 3, horizontal flue 4 and the back-end ductwork 5 that are connected successively, and is arranged at the soot blower 6 on radiant cooling room 3, horizontal flue 4 and back-end ductwork 5;
The end face of descending adiabatic furnace 1 is provided with Waste liquid atomization spray gun 11 and root wind snout 12, and top is provided with assisted gas burner I 13, and middle part is provided with assisted gas burner II 14, Hou Qiang bottom and is provided with furnace arch, furnace nose 15;
The porch of radiant cooling room 3 is provided with screen tube 31, and top is provided with E font water-cooling screen 32;
Horizontal flue 4 is provided with convection current screen 41;
Back-end ductwork 5 is disposed with II grade of economizer 51, plate air preheater 52 and I grade of economizer 53 from the inlet to the outlet, and the air outlet slit of plate air preheater 52 is connected with root wind snout 12;
The partial fume in II grade of economizer 51 exit is recycled, enters descending adiabatic furnace 1 and radiant cooling room 3 as adherent protection flue gas; Between descending adiabatic furnace 1 and radiant cooling room 3, junction is V-arrangement angle 2, and the sidewall of V-arrangement angle 2 is water-cooling wall 21, water-cooling wall 21 is equipped with refractory material 22, and the bottom of V-arrangement angle 2 is liquid state slag discharging device 23.
The carbonated drink outlet of I grade of economizer, 53, II grade of economizer 51, water-cooling wall 21, E font water-cooling screen 32, convection current screen 41 is connected with drum 9 with carbonated drink fairlead 8 by header 7, drum 9 is connected with down-comer 10, and the outlet of the carbonated drink of down-comer 10 shields 41 again carbonated drink entrance with water-cooling wall 21, E font water-cooling screen 32, convection current is connected.
According to the technical solution of the utility model, be an embodiment with certain factory 37t/h liquid waste incineration boiler, the low 8m of aspect ratio radiant cooling room 3 of descending adiabatic furnace 1, refractory material 22 laying place is 3m with the distance bottom V-arrangement angle 2, and the interior angle of V-arrangement angle 2 is 60 °.Containing the hazardous waste such as flammable explosive gas and spent lye compositions such as various low-boiling-point substance, high-boiling components in waste liquid, its characteristic embodies a concentrated expression of following two aspects: low heat value, low ash smelting point.Design liquid waste processing amount is 16.8t/h, and combustion-supporting fuel adopts natural gas, and calorific value is about 35800kJ/Nm
3, the amount of natural gas of required afterburning is about 1400Nm
3/ h, steam parameter is 1.37MPa, 174 DEG C, byproduct steam 37t/h.
Concrete operations are as follows: waste liquid sprays into descending adiabatic furnace 1 from Waste liquid atomization spray gun 11 atomization, and air is sprayed into by root wind snout 12, and natural gas sprays into from assisted gas burner I 13 and assisted gas burner II 14, and in two-layer corner tangential firing; The assisted gas burner I 13 of upper furnace is oxygen deprivation fuel-rich regions, and temperature controls at about 500 DEG C, and assisted gas burner II 14 region, middle part is combustion zone, and ignition temperature, at about 1200 DEG C, ensures the complete after-flame of waste liquid.Burner hearth internal classification air distribution, sprays into flue gas recycled below two-layer burner, controls primary zone oxygen amount and temperature.And flue gas recycled is divided into level Four (I grade of adherent protection flue gas 16 as adherent protection flue gas, II grade of adherent protection flue gas 17, III grade of adherent protection flue gas 24, IV grade of adherent protection flue gas 25, adherent protection flue gas accounts for 20% of total exhaust gas volumn) adherently along flow of flue gas direction spray into descending adiabatic furnace 1 and radiant cooling room 3, waste liquid and liquid slag contacting and corrosion furnace wall is suppressed by the airflow layer of flue gas stroke, form hypothermia and hypoxia region, adherent liquid slag cooled and solidified is formed the solid-state slag blanket of protectiveness in furnace wall, prevent liquid slag from directly contacting furnace wall.Flue gas is descending in burner hearth, swerves through V-arrangement angle 2, enters radiant cooling room 3, and further catch slag and deslagging by screen tube 31 to liquid slag after carrying out inertial separation.The exit gas temperature of screen tube 31 is about 1050 DEG C, drops to about 650 DEG C by flue-gas temperature after radiant cooling room 3 and E font water-cooling screen 32; Flue gas enters horizontal flue 4, by convection current screen 41 cooling, makes flue gas drop to about 550 DEG C; Enter back-end ductwork 5 again, make temperature drop to about 500 DEG C by II grade of economizer 51; Flue gas is by plate air preheater 52 and air heat-exchange, and flue-gas temperature drops to about 300 DEG C further, and the air after intensification enters descending adiabatic furnace 1 by root wind snout 12 and participates in burning; Flue gas drops to about 200 DEG C finally by I grade of economizer 53 temperature; Flue gas after cooling enters the flue gas processing device of next stage again.
In liquid waste incineration process, the main component of ash is sodium carbonate, and its fusing point is 853 DEG C, and under combinational environment, its fusing point will be reduced to 600 DEG C ~ 750 DEG C.Recovery has two kinds of forms: the preliminary cooling being first through water-cooling wall 21 is flowed out from liquid state slag discharging device 23 with molten, fused mass enters cooling in molten groove and forms solid slag, recycling submerged slag conveyor is pulled out and is delivered to slag storehouse, and its yield accounts for 50% ~ 60% of overall recovery; Secondly, the ash of being discharged by boiler tail reclaims in solid form (first to be removed the dust stratification on boiler heating surface by soot blower 6, again by being arranged on ash bucket after horizontal flue 4 and back-end ductwork 5 and electric precipitation collects dust, do not provide in FIG), water-cooling wall arranged by ash bucket, cooling lime-ash, avoids the formation of compactness slag blanket.
Concrete flue gas flow is: the 53 → outlet of capable water-cooling screen 32 → convection current screen 41 → II grades of economizer 51 (partial fume enters burner hearth through the flue gas recirculation) → plate air preheaters of descending adiabatic furnace 1 → V-arrangement angle 2 → radiant cooling room 3 → E word 52 → I grades of economizers.Concrete air flow process is: plate air preheater 52 → root wind snout 12 → descending adiabatic furnace 1.Concrete carbonated drink flow process is: → I grade of economizer 53 → II grades of economizer 51 → drum 9 → down-comer 10 → water-cooling walls 21 that feed water, the capable water-cooling screen 32 of E word, convection current screen 41 → drum 9.
Above content is only to detailed description of the invention example of the present utility model and explanation; what should indicate is; according to conception of the present utility model above-mentioned embodiment modified or supplement or adopt similar mode to substitute; its function produced do not exceed that description and accompanying drawing contain yet spiritual time, all should within protection domain of the present utility model.
Claims (7)
1. the liquid waste incineration boiler of the adherent protection of flue gas recycled, described burning boiler comprises the descending adiabatic furnace, radiant cooling room, horizontal flue and the back-end ductwork that are connected successively, and is arranged at the soot blower on radiant cooling room, horizontal flue and back-end ductwork;
The end face of described descending adiabatic furnace is provided with Waste liquid atomization spray gun and root wind snout, and top is provided with assisted gas burner I, and middle part is provided with assisted gas burner II, Hou Qiang bottom and is provided with furnace arch, furnace nose;
The porch of described radiant cooling room is provided with screen tube, and top is provided with E font water-cooling screen;
Described horizontal flue is provided with convection current screen;
Described back-end ductwork is disposed with II grade of economizer, plate air preheater and I grade of economizer from the inlet to the outlet, and the air outlet slit of plate air preheater is connected with root wind snout;
It is characterized in that: the partial fume at II grade of economizer exit place is recycled, enters descending adiabatic furnace and radiant cooling room as adherent protection flue gas; Between described descending adiabatic furnace and radiant cooling room, junction is V-arrangement angle, and the sidewall of V-arrangement angle is water-cooling wall, and water-cooling wall is equipped with refractory material, and the bottom of V-arrangement angle is liquid state slag discharging device.
2. the liquid waste incineration boiler of the adherent protection of a kind of flue gas recycled according to claim 1, is characterized in that: the low 6 ~ 10m of aspect ratio radiant cooling room of described descending adiabatic furnace.
3. the liquid waste incineration boiler of the adherent protection of a kind of flue gas recycled according to claim 1, is characterized in that: laying place of described refractory material is 3 ~ 5m with the distance bottom V-arrangement angle.
4. the liquid waste incineration boiler of the adherent protection of a kind of flue gas recycled according to claim 1, is characterized in that: the interior angle of described V-arrangement angle is 60 ° ~ 90 °.
5. the liquid waste incineration boiler of the adherent protection of a kind of flue gas recycled according to claim 1, is characterized in that: described screen tube is arranged by four the Crust blocks pipe bundle be staggered in arrangement and formed.
6. the liquid waste incineration boiler of the adherent protection of a kind of flue gas recycled according to claim 1, is characterized in that: between the screen of described E font water-cooling screen, spacing is greater than 400mm.
7. the liquid waste incineration boiler of the adherent protection of a kind of flue gas recycled according to claim 1; it is characterized in that: the carbonated drink outlet of described I grade of economizer, II grade of economizer, water-cooling wall, E font water-cooling screen, convection current screen is connected with drum with carbonated drink fairlead by header; drum is connected with down-comer, and the carbonated drink entrance that the carbonated drink outlet of down-comer is shielded with water-cooling wall, E font water-cooling screen, convection current is again connected.
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| CN201520196432.4U CN204534605U (en) | 2015-04-02 | 2015-04-02 | The liquid waste incineration boiler of the adherent protection of a kind of flue gas recycled |
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Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104764025A (en) * | 2015-04-02 | 2015-07-08 | 北京华电光大装备技术有限公司 | Waste liquid incineration boiler of recycling smoke adherence protection |
| CN105910115A (en) * | 2016-04-19 | 2016-08-31 | 中石化炼化工程（集团）股份有限公司 | Waste liquid incineration device |
| CN115371061A (en) * | 2022-10-26 | 2022-11-22 | 浙江百能科技有限公司 | High-concentration salt-containing organic waste liquid incineration device and incineration molten slag separation and recovery process |
-
2015
- 2015-04-02 CN CN201520196432.4U patent/CN204534605U/en active Active
Cited By (3)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104764025A (en) * | 2015-04-02 | 2015-07-08 | 北京华电光大装备技术有限公司 | Waste liquid incineration boiler of recycling smoke adherence protection |
| CN105910115A (en) * | 2016-04-19 | 2016-08-31 | 中石化炼化工程（集团）股份有限公司 | Waste liquid incineration device |
| CN115371061A (en) * | 2022-10-26 | 2022-11-22 | 浙江百能科技有限公司 | High-concentration salt-containing organic waste liquid incineration device and incineration molten slag separation and recovery process |
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